Low molecular weight oligomeric coagulation aid and dispersion aid

ABSTRACT

A composition for dispersing multilayer polymers has an oligomer prepared from at least one alkyl (meth)acrylate monomer in the presence of a chain transfer agent. The oligomer has a number average molecular weight of less than 2,500 g/mol. A composition containing the oligomer and a multilayer polymer, such as an acrylic core-shell polymer or methacrylate butadiene styrene core-shell polymer, and a resin composition are also disclosed.

FIELD OF THE INVENTION

The present invention generally relates to a composition and, more specifically, to a composition for dispersing multilayer polymers.

DESCRIPTION OF THE RELATED ART

Multilayer (e.g., core-shell) polymers or rubbers are a commonly used plastic additive used to improve the properties of compositions, such as, (meth) acrylic resins (e.g., methyl methacrylate (MMA)) and epoxy resins. Without an additive, such resins are often too brittle to be of use. For example, acrylic multilayer polymers and methacrylate butadiene styrene (MBS) core-shell polymers are often added to resins to substantially improve the impact strength of plastic compositions.

Due to ease of handling and processing, multilayer polymers are typically supplied and added to compositions in the form of a powder. These powdered multilayer polymers can be prepared by conventional emulsion polymerization and isolated to powders by spray drying or coagulation to produce the desired powder size. When added to plastic compositions, these agglomerated multilayer polymers are intended to disperse throughout the plastic composition. However, the powdered multilayer polymers do not often disperse as desired and have a high dispersion viscosity.

Attempts to improve the dispersion of multilayer polymers in the resin compositions have been made. For MBS core-shell polymers, one approach is to increase the level of the shell, i.e., increase the ratio of the shell with respect to the core, which is made mostly from MMA. While increasing the MMA shell levels improves dispersibility, a higher coagulation temperature also results from the higher MMA shell levels.

The use of certain multilayer polymers alone, including MBS core-shell polymers, especially ones made with high MMA shell levels, can also lead to high coagulation temperatures. High coagulation temperatures result in higher energy costs and increased cycle times for preparing the compositions.

WO 2017/121749 discloses a liquid composition comprising a (meth)acrylic polymer, a multi-stage polymer, and a monomer where the (meth)acrylic polymer has a mass average molecular weight, Mw, of less than 100,000 g/mol. The (meth)acrylic polymer comprises essentially polymers comprising (meth) acrylic monomers that make up 50 wt % or more of the (meth) acrylic polymer.

There is a need for an additive that can provide good dispersibility while lowering the coagulation temperature. The present invention seeks to address one or more of these problems.

BRIEF SUMMARY OF THE INVENTION

The present invention provides a composition for dispersing core shell particles, the composition comprising an oligomer prepared from at least one alkyl (meth)acrylate monomer in the presence of a chain transfer agent, wherein the oligomer has a number average molecular weight of less than 2,500 g/mol.

The present invention also relates to a composition comprising a multilayer polymer and an oligomer prepared from at least one alkyl (meth)acrylate monomer in the presence of a chain transfer agent, wherein the oligomer has a number average molecular weight of less than 2,500 g/mol and a T_(g) of less than −10° C. as measured by DSC.

DETAILED DESCRIPTION OF THE INVENTION

The present invention provides a composition for dispersing multilayer polymers. The present inventors have unexpectedly discovered that a low molecular weight oligomer additive can result in the significant improvement in the dispersion of multilayer polymers in resins, such as epoxy and alkyl (meth)acrylate monomers, such as methyl methacrylate. Additionally, the oligomer additive can provide significant improvements in the coagulation temperature.

One aspect of the present invention relates to a composition for dispersing multilayer polymers comprising a low molecular weight oligomer.

As used herein, an “oligomer” is distinguished from a polymer in that an oligomer has relatively few monomeric units and has minimal, if any, chain entanglements due to its shorter length. Polymers exhibit polymer-like properties, such as film and fiber forming, and the addition or removal of one or a few of the units has a negligible effect on the properties. Quantitatively, an oligomer according to the present invention has a number average molecular weight of less than 2,500 g/mol. This definition is consistent with the definition provided by Naka K. (2014) Monomers, Oligomers, Polymers, and Macromolecules (Overview). In: Kobayashi S., Müllen K. (eds) Encyclopedia of Polymeric Nanomaterials. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-36199-9_237-1, which defines a polymer as having a molecular weight greater than 10,000 g/mol.

Preferably, the oligomer has a number average molecular weight, M_(n), less than 2,500 g/mol. More preferably, the oligomer has a number average molecular weight less than 2,250 g/mol, even more preferably less than 2,000 g/mol, such as, for example, less than 1,900 g/mol, less than 1,800 g/mol, less than 1,750 g/mol, less than 1,700 g/mol, or less than 1,650 g/mol. Size Exclusion Chromatography (SEC) with refractive index (RI) detection in THF was used to determine molecular weight distribution of oligomers. Poly(methyl methacrylate) (PMMA) standards were used to determine relative molecular weight data of oligomers. Samples were prepared in duplicate by diluting the samples into THF at a concentration of around 2 mg/ml. The sample-solvent mixtures were shaken on a mechanical shaker for 2 hours at room temperature, rested overnight, and then filtered using a 0.45 μm PTFE filter prior to the GPC analysis. SEC separations were carried out on an Agilent 1260 Infinity II Model (in RTG-CV) consisting of an isocratic pump, multicolumn thermostat, integrated degasser, auto sampler, and refractive index detector. Agilent GPC/SEC software Version A.02.01; Build 9.34851 were used to process the data. The Gel permeation chromatography (GPC) separation was performed in THF at a flow rate of 1 mL/min using a GPC column set composed of two PLgel columns Mixed D columns (300×7.5 mm ID) and a guard column in series (particle size 5 μm). The sample injection volume was 100 μL.

The oligomer is prepared from at least one alkyl (meth)acrylate monomer in the presence of a chain transfer agent. The oligomer can be prepared, for example, by emulsion polymerization of the monomers in the presence of the chain transfer agent.

The low molecular weight oligomer may have a glass transition temperature T_(g) of less than 75° C. as measured by differential scanning calorimetry (DSC) at 10° C./minute. Due to the low molecular weight of the oligomers according to the present invention, the T_(g) of the oligomer, as measured by DSC, can vary significantly from the T_(g) calculated with the Fox equation [Bulletin of the American Physical Society 1, 3 Page 123 (1956)]. The Fox equation calculates the T_(g) as follows:

$\frac{1}{T_{g}} = {\frac{w_{1}}{T_{g(1)}} + \frac{w_{2}}{T_{g(2)}}}$

In the Fox equation, w₁ and w₂ refer to the weight fraction of the two comonomers, based on weight of monomers charged to the reaction vessel, and T_(g(1)) and T_(g(2)) refer to the glass transition temperatures of the two corresponding homopolymers in degrees Kelvin. When three or more monomers are present, additional terms are added (w_(n)/T_(g (n))). The glass transition temperatures of homopolymers for the purposes of this invention are those reported in “Polymer Handbook”, edited by J. Brandrup and E. H. Immergut, Interscience Publishers, 1966, unless that publication does not report the Tg of a particular homopolymer, in which case the Tg of the homopolymer is measured by DSC.

Surprisingly, it has been discovered that oligomers formed from monomers that would have a relatively high T_(g) (e.g., methyl methacrylate monomers) compared to monomers that would have a relatively low T_(g) (e.g., butyl acrylate, ethyl acrylate, or butyl methacrylate) still exhibit significant reductions in coagulation temperature and improved dispersion when coagulated with a multilayer polymer.

Alkyl (meth)acrylate monomers that may be used in the preparation of the oligomer include, but are not limited to ethyl (meth)acrylate, ethyl hexyl (meth)acrylate, methyl (meth)acrylate, glycidyl methacrylate, butyl (meth)acrylate, lauryl (meth)acrylate, poly(ethylene glycol) methacrylate, and 1,3-butylene glycol dimethacrylate. As used herein, “alkyl (meth)acrylate” refers to both the alkyl acrylate and the alkyl methacrylate.

In addition to the at least one alkyl (meth)acrylate monomer, additional monomers may also be used to prepare the oligomer. For example, the oligomer may be prepared from at least one alkyl (meth)acrylate monomer and an additional monomer. The additional monomer may be selected from, for example, styrene monomers and acrylamide monomers, such as, for example, dimethyl acrylamide and diacetone acrylamide.

The degree of polymerization of the oligomer is less than 25. Preferably, the degree of polymerization is less than 20. As used herein, the degree of polymerization is calculated based on the molar ratio of chain transfer agent to monomers in the reaction mixture, assuming 1 terminal chain transfer agent residue per chain.

The chain transfer agent (CTA) may be any compound known or found to be useful as a chain transfer agent in polymerization of acrylate or methacrylate monomers. For example, thiol chain transfer agents can be used. Examples of such thiol CTAs include, but are not limited to, propyl mercaptan, butyl mercaptan, methyl mercaptan, hexyl mercaptan, octyl mercaptan, dodecyl mercaptan, tetra-thiol thioglycollic acid, mercaptopropionic acid, alkyl thioglycollates e.g., 2-ethyl hexyl thioglycollate (EHTG) or octylthioglycollate, mercaptoethanol, mercaptoundecanoic acid, thiolactic acid, thiobutyric acid, trimethylol propane tris(3-mercaptopropionate), pentaerythritol tetra(3-mercaptopropionate), pentaerythritol tetrathioglycollate, pentaerythritol tetrathiolactate, pentaerythritol tetrathiobutyrate; methyl 3-mercaptopropionate (MMP), butyl 3-mercaptopropionate (BM P), pentaerythritol tetrakis(3-mercaptopropionate) (PETMP), dipentaerythritol hexa(3-mercaptopropionate), dipentaerythritol hexathioglycollate; tripentaerythritol octa(3-mercaptopropionate), and tripentaerythritol octathioglycollate. The use of polyfunctional thiols is a useful way to increase the degree of branching in the polymer. Optionally, the chain transfer agent may comprise a mixture of more than one type of compound. Preferably, the CTA comprises MMP, BMP, PETMP, EHTG, or a mixture thereof. More preferably, the CTA comprises BMP or a mixture thereof.

The oligomer may be prepared by any known method. Preferably, the oligomer is prepared by emulsion polymerization.

A further aspect of the present invention relates to a composition comprising a multilayer polymer, such as, for example, a core-shell polymer and the oligomer. Preferably, the composition comprising the multilayer polymer and the oligomer is coagulated and dried to form a powder.

The multilayer polymer may comprise an acrylic core-shell polymer or a MBS core-shell polymer. Acrylic core-shell polymers may include, for example, an acrylic core-shell polymer having a core comprising butyl acrylate and a shell comprising methyl methacrylate, and optionally, one or more intermediate layers between the core and the shell. The MBS core-shell polymer may comprise, for example, a crosslinked butadiene core covered with a grafted and optionally crosslinked methyl methacrylate shell. The MBS core-shell polymer may optionally comprise an intermediate layer between the core and the shell, where the intermediate layer is a highly crosslinked layer between the core and the shell, e.g., a layer made from methyl methacrylate monomers and 1,3-butylene glycol dimethacrylate monomers. The composition can be prepared by blending an emulsion of the oligomer and an emulsion containing the multilayer polymer, or the oligomer can be synthesized in situ in the presence of a multilayer polymer emulsion prior to coagulation.

Preferably, a composition comprising a multilayer polymer and an oligomer of the present invention results in a coagulation temperature of less than 80° C., more preferably less than 75° C., and even more preferably less than 70° C. As used herein, the “coagulation temperature” is the temperature where a composition comprising the oligomer and a multilayer polymer is coagulated, resulting in a coagulate that has an average particle diameter of 200 microns. The coagulation temperature can be interpolated or extrapolated for an average particle diameter by measuring the coagulation temperature of different sized particles.

Oligomers of the present invention lower the coagulation temperature. Without wishing to be bound by theory, it is believed that the oligomer acts as an adhesive to bind the core-shell polymer into powder grains, thus enabling a harder shell and increased shell thickness on the core-shell polymer, which also tends to favor dispersion when added to a resin composition. Without the oligomer, increases in the ratio of the shell relative to the core are limited by the coagulation temperature. The composition may be prepared by cold blending the oligomer emulsion with a core-shell polymer emulsion prior to coagulation. The resulting mixture can then be isolated and dried to form a powder comprising the core-shell polymer and the oligomer.

The oligomer may be present in the powder composition in an amount ranging from 1 to 98 wt % relative to the total weight of the powder composition. Preferably, the oligomer is present in the powder composition in an amount of at least 2 wt %, at least 3 wt %, at least 4 wt %, or at least 5 wt % relative to the total weight of the powder composition. Preferably, the oligomer is present in an amount less than 80 wt %, less than 60 wt %, less than 50 wt %, less than 40 wt %, less than 30 wt %, or less than 20 wt %.

The powder preferably has an average particle diameter ranging from 50 to 500 microns. More preferably, the powder has an average particle diameter ranging from 75 to 400 microns, such as, from 100 to 300 microns. Even more preferably, the powder has an average particle diameter ranging from 150 to 250 microns As used herein the phrase “average particle diameter” or “average particle size” is the arithmetic mean of all possible diameters, where a diameter is any linear dimension passing through the center of the particle. The particle size of the oligomers was measured on a Malvern Zetasizer Nano S90 particle size analyzer.

The oligomer of the present invention may also result in significant reduction in the viscosity when used in liquid resin compositions, such as epoxy and methyl methacrylate resins.

Another aspect of the present invention relates to resin compositions comprising or prepared from the powder compositions according to the present invention. For example, the resin composition may comprise an epoxy resin or a methyl methacrylate resin which is blended with the powder of the present invention, which comprises a multilayer polymer, such as, for example, a MBS or acrylic core-shell polymer, and an oligomer additive.

The powder comprising the multilayer polymer and the oligomer additive may be added to the resin composition in an amount ranging from 2 to 30 wt % relative to the total weight of the resin composition, preferably from 5 to 25 wt % relative to the total weight of the resin composition. The oligomer additive may be present in the resin composition in an amount ranging from 0.5 to 10 wt %, such as, for example, from 2 to 8 wt %, or from 4 to 6 wt % relative to the total weight of the resin composition. Resin compositions according to the present invention have improved dispersion relative to similar resin compositions that do not contain the oligomer. As used herein, “improved dispersion” means that the resin composition is more homogeneous and does not contain visible particles or agglomerations of the powder. Alternatively, when used in liquid resin compositions, the resin compositions have a lower viscosity compared to resin compositions that do not contain the oligomer.

Alternatively, the powder composition of the multilayer polymer and the oligomer additive may be combined with another powder comprising a multilayer polymer and no oligomer additive. For example, the powder composition comprising the multilayer polymer and the oligomer additive may comprise a relatively higher amount of the oligomer additive that is blended with another powder to adjust the total amount of oligomer additive in the resulting resin composition. The proportions of the oligomer additive present in the powder composition can therefore be higher and adjusted through the use of a second powder that does not comprise the oligomer additive.

The present invention further relates to a process for improving the dispersion of a multilayer polymer comprising adding a powder composition comprising the multilayer polymer and the oligomer additive to a resin composition, where the dispersion of the multilayer polymer is improved compared to a similar composition made with a powder composition that does not comprise the oligomer additive.

EXAMPLES

Oligomers according to the present invention were prepared by conventional emulsion polymerization based on the formulations in Table 1. The oligomers had a very low T_(g). Oligomer 1 was formed by the following process. To a 5 liter, 4-necked round bottomed flask equipped with a mechanical stirrer, thermometer, condenser, and electric heating mantel, was charged 1497.02 g of deionized water, 0.094 g of Sequestrene and 10.27 g of a 28% aqueous solution of sodium lauryl sulfate surfactant. The reactor contents were heated to 80° C. In a separate container 125 g of butyl 3-mercaptopropionate, 112.5 g of methyl methacrylate, 1012.5 g of butyl acrylate, 56.70 g of a 28% aqueous solution of sodium lauryl sulfate, and 275.65 g of deionized water were blended and agitated to form a monomer emulsion mixture. 79.12 g of the monomer emulsion mixture was added to the reactor, followed by simultaneous feeds of 100 g of 2.5% aqueous solution of t-butyl hydroperoxide and 100 g of 2.5% aqueous solution of sodium formaldehyde sulfoxylate at flow rates of 1.11 g/minute, respectively. After 15 minutes, the rest of the monomer emulsion mixture was added at a flow rate of 33.41 g/minute. At the end of the feeds the reactor was cooled to 40° C. and filtered, and no coagulum was observed. The polymer solids content was measured to be 38.2% and the emulsion latex particle size was measured to be 105 nm.

TABLE 1 Oligomer Weight % Target Measured ID BA MMA BMP DP M_(n)* Mn Olig. 1 81.0 9.0 10.0 12 1623 1500 ± 100 Olig. 2 83.25 9.25 7.5 21 2163 1800 ± 100 *The measured M_(n) was within +/− 10% of the target M_(n).

The oligomer emulsions produced in accordance with Table 1 were cold blended with an MBS core-shell polymer emulsion, isolated, and dried to form a powder. The MBS core-shell polymer comprised 72 wt % butadiene core and a 28 wt % methyl methacrylate shell where the weight percentages are based on the total weight of the MBS core-shell polymer. To prepare the MBS core-shell polymer, a stainless steel autoclave with an agitator and several entry ports was charged 6300 parts of deionized water, 170 parts of a 60 nm polymer preform and 4 parts of potassium oleate. After evacuating the reactor, 3200 parts of butadiene, 4 parts of divinylbenzene, 37 parts of diisopropylbenzene hydroperoxide, 11 parts of sodium formaldehyde sulfoxylate and 30 additional parts of potassium oleate were added and the mixture was allowed to react at 65° C. until there was no longer a drop in pressure. The reaction vessel was then vented to remove any remaining volatile material.

To 2000 parts of the rubber latex having approximately 34% solids, as prepared above, were added 0.59 parts of sodium formaldehyde sulfoxylate dissolved in 10 parts of deionized water and 0.51 parts of 70% active strength tert-butyl hydroperoxide in 6 parts of deionized water, followed a monomer mixture of 181 parts of methyl methacrylate, 3.8 parts of styrene, 3.2 parts of divinyl benzene over 1 hour. After the end of the monomer mixture feed, 0.3 parts of sodium formaldehyde sulfoxylate dissolved in 5 parts of deionized water and 0.25 parts of 70% active strength tert-butyl hydroperoxide in 3 parts of deionized water were added, followed by a monomer mixture of 46.9 g MMA and 11.7 g BA over 20 minutes. 5 minutes after the completion of the feeds, 0.3 parts of sodium formaldehyde sulfoxylate dissolved in 5 parts of deionized water and 0.25 parts of 70% active strength tert-butyl hydroperoxide in 3 parts of deionized water were added. 30 minutes after the end of the feeds, 0.36 parts of sodium formaldehyde sulfoxylate dissolved in 72 parts of deionized water and 0.3 parts of 70% active strength tert-butyl hydroperoxide dissolved in 42 parts of deionized water were added over 180 minutes and caused to react to completion. The resulting multistage polymer latex had approximately 38% solids.

To prepare Coagulation 1, to a quart size flask were added 25.4 g of the oligomer 1 emulsion with solid content of 41.8%, 534.6 g MBS core shell polymer emulsion with solid content of 37.4%, followed by 139 g deionized water. The mixture was heated to 63° C.

An antioxidation emulsion preparation was prepared by adding 4.51 g potassium oleate, 2.45 g BNX® DLTDP, 2.45 g butylated hydroxytoluene, 0.6 g Irganox 245, and 16.8 g deionized water to a 250 ml plastic container. The mixture was homogenized at 10000 rpm for 10 minutes.

To coagulate the composition, 3.6 g of 3% hydrochloric acid aqueous solution, 0.67 g of 0.05% calcium chloride aqueous solution, and 1309.1 g deionized water were added to a 3 liter beaker. The beaker content was heated to 63° C. under agitation at 500 rpm. When the content reached 63° C., the preheated emulsion above was added slowly over 30-45 seconds to the beaker. This caused phase separation of the mixture into a water phase and a solid polymer phase. 70.7 g of 3% hydrochloric acid aqueous solution was added to complete the coagulation. The contents of the beaker were then neutralized to pH of 7.0 using 63 g of 5% sodium hydroxide aqueous solution. The mixture was then heated to 90° C., and held at 90° C. for 30 minutes. After the hold, the mixture was cooled, dewatered, and washed in a Büchner funnel. The samples were washed with deionized water until the filtrate conductivity is below 30 μS/m, and then dewatered. The samples were dried in a vacuum oven for overnight at 40° C. The particle size of the powder was measured on a Malvern Mastersizer 2000.

The oligomer was added in an amount of 5 wt % relative to the total weight of MBS core-shell polymer and the oligomer. As shown in Table 2, the addition of the oligomer significantly decreased the coagulation temperature of the composition.

TABLE 2 Coagulation Temp. Particle Extrapolated MBS Oligomer Coagulation Size to 200 μm Sample (wt %) (wt %) Temp.* (μm) Particle Size Control 1 100%  0% 73° C. 221 72.1° C. Coag. 1 95% 5% Olig. 1 63° C. 233 61.8° C. Coag. 2 95% 5% Olig. 2 63° C. 199   63° C. *Coagulation temperature for the actual particle size produced.

To test the dispersibility of the coagulated MBS core-shell/oligomer, the coagulated composition was added to either an epoxy resin (D.E.R.™-331 epoxy resin available from Olin Corporation) or methyl methacrylate monomers.

To prepare MMA dispersions, 12 g of polymer was slowly added to a mixing cup containing 38 g of methyl methacrylate at room temperature. The resulting mixture was hand mixed with a spatula, then agitated with a mixer at 1600 rpm for 60 seconds. The resulting dispersion was spread down on a Leneta chart for visual inspection of dispersion quality. The dispersion viscosity was measured on a Brookfield model DV-I+viscometer at shear rate of 5 rpm.

To prepare the epoxy dispersions, a resin kettle containing 249 g D.E.R. 331 epoxy resin was heated to 60° C. With an agitation rate of 1800 rpm, 51 g polymer powder was added to the kettle. The kettle content was agitated for 90 min and then cooled down to room temperature. The resulting dispersion were spread down for visual inspection of dispersion quality. The dispersion viscosity was measured on a Brookfield model DV-II viscometer at shear rate of 0.3 rpm at room temperature.

TABLE 3 Viscosity Resin Powder (cP @ Sample (wt %) (wt %) Observations 0.3 rpm) Comp. Ex. 1 83% Epoxy 17% Control 1 Gritty 240000 Ex. 1 83% Epoxy 17% Coag. 1 No grit 68000 Ex. 2 83% Epoxy 17% Coag. 2 No grit 64000 Comp. Ex. 2 75% MMA 25% Control No grit 210000 Ex. 3 75% MMA 25% Coag. 1 No grit 20000 Ex. 4 75% MMA 25% Coag. 2 No grit 105000

In each of the examples incorporating an oligomer according to the present invention, the final composition had a significantly improved viscosity and appearance. The dispersion of Comparative Example 1 was poor and the sample had undispersed grit and a high viscosity. The examples according to the present invention exhibited excellent dispersion with no grit, had low viscosity, as well as the lowered coagulation temperature in the formation of the MBS latex.

Another set of experiments were performed to determine the effect of the composition of the oligomer. A series of oligomers was prepared according to Table 4. These oligomers were prepared in the same manner as those described above in Table 1.

TABLE 4 Oligomer Weight % Target ID BA BMA MMA BMP DP M_(n)* Olig. 3 90%  0%  0% 10% 12.4 1623 Olig. 4  0% 90%  0% 10% 11.3 1623 Olig. 5  0% 75% 15% 10% 12.0 1623 Olig. 6  0% 60% 30% 10% 12.7 1623 Olig. 7  0% 45% 45% 10% 13.4 1623 Olig. 8  0% 30% 60% 10% 14.1 1623 Olig. 9  0% 15% 30% 10% 14.9 1623 Olig. 10  0%  0% 90% 10% 15.6 1623 *The measured M_(n) was within +/− 10% of the target M_(n).

Table 5 shows the glass transition temperature calculated with the Fox equation and the experimentally determined glass transition temperature using DSC, as well as the difference between the calculated T_(g) and the measured T_(g) (Fox−DSC). The substantial difference between the calculated T_(g) and the measured T_(g) is indicative of the oligomeric nature of the additive.

TABLE 5 Oligomer DSC Tg (° C.) DSC (° C.) Fox − DSC ID Fox Tg (° C.) Replicates Average (° C.) Olig. 3 −50 −69 −68 −69 19 Olig. 4 20 −39 −32 −36 56 Olig. 5 31 −24 −26 −25 56 Olig. 6 44 −10 −8 −9 53 Olig. 7 57 2 3 3 55 Olig. 8 72 15 18 17 56 Olig. 9 88 21 27 24 64 Olig. 10 105 44 43 44 62

The oligomers Olig. 3 to 10, produced in accordance with Table 4, were cold blended with an MBS core-shell polymer emulsion, isolated, and dried to form a powder. The MBS core-shell polymer comprised 77 wt % butadiene core and a 23 wt % methyl methacrylate shell, where the weight percentages are based on the total weight of the MBS core-shell polymer. The oligomer was added in an amount of 5 wt % relative to the total weight of MBS core-shell polymer and the oligomer. As shown in Table 6, the addition of the oligomer significantly decreased the coagulation temperature of the composition.

TABLE 6 Coagulation Temp. Extrapolated MBS Oligomer to 200 μm Particle Sample (wt %) (wt %) Particle Size Size (μm)* Control 2 100%  0% 55.2° C. 222 Coag. 3 95% 5% Olig. 3 50.1° C. 197 Coag. 4 95% 5% Olig. 4 51.1° C. 173 Coag. 5 95% 5% Olig. 5 45.8° C. 205 Coag. 6 95% 5% Olig. 6 41.3° C. 555 Coag. 7 95% 5% Olig. 7 43.4° C. 353 Coag. 8 95% 5% Olig. 8 47.0° C. 293 Coag. 9 95% 5% Olig. 9 44.8° C. 380 Coag. 10 95%  5% Olig. 10 46.3° C. 317 *Particle size is measurement of actual average particle diameter of particles formed.

The coagulated powders, Coag. 3 to 10, at a concentration of 17 wt % relative to the total weight of the composition, were dispersed in epoxy (D.E.R.™-331 epoxy resin) and the observations are reported in Table 7.

TABLE 7 Dispersion Sample Epoxy (wt %) Powder (wt %) Observations Comp. Ex. 3 83% 17% Control 2 Poor Ex. 5 83% 17% Coag. 3 Excellent Ex. 6 83% 17% Coag. 4 Excellent Ex. 7 83% 17% Coag. 5 Excellent Ex. 8 83% 17% Coag. 6 Excellent Ex. 9 83% 17% Coag. 7 Excellent Ex. 10 83% 17% Coag. 8 Excellent Ex. 11 83% 17% Coag. 9 Excellent Ex. 12 83% 17% Coag. 10 Excellent

As seen in Tables 6 and 7, the oligomers according to the present invention provided both an improved dispersion and a reduced coagulation temperature.

Unless otherwise indicated by the context of the specification, all amounts, ratios and percentages are by weight, and all test methods are current as of the filing date of this disclosure. The articles “a”, “an” and “the” each refer to one or more. It is to be understood that the appended claims are not limited to express and particular compounds, compositions, or methods described in the detailed description, which may vary between particular embodiments which fall within the scope of the appended claims. With respect to any Markush groups relied upon herein for describing particular features or aspects of various embodiments, different, special, and/or unexpected results may be obtained from each member of the respective Markush group independent from all other Markush members. Each member of a Markush group may be relied upon individually and or in combination and provides adequate support for specific embodiments within the scope of the appended claims.

Further, any ranges and subranges relied upon in describing various embodiments of the present invention independently and collectively fall within the scope of the appended claims, and are understood to describe and contemplate all ranges including whole and/or fractional values therein, even if such values are not expressly written herein. One of skill in the art readily recognizes that the enumerated ranges and subranges sufficiently describe and enable various embodiments of the present invention, and such ranges and subranges may be further delineated into relevant halves, thirds, quarters, fifths, and so on. As just one example, a range “of from 0.1 to 0.9” may be further delineated into a lower third, i.e., from 0.1 to 0.3, a middle third, i.e., from 0.4 to 0.6, and an upper third, i.e., from 0.7 to 0.9, which individually and collectively are within the scope of the appended claims, and may be relied upon individually and/or collectively and provide adequate support for specific embodiments within the scope of the appended claims. In addition, with respect to the language which defines or modifies a range, such as “at least,” “greater than,” “less than,” “no more than,” and the like, it is to be understood that such language includes subranges and/or an upper or lower limit. As another example, a range of “at least 10” inherently includes a subrange of from at least 10 to 35, a subrange of from at least 10 to 25, a subrange of from 25 to 35, and so on, and each subrange may be relied upon individually and/or collectively and provides adequate support for specific embodiments within the scope of the appended claims. Finally, an individual number within a disclosed range may be relied upon and provides adequate support for specific embodiments within the scope of the appended claims. For example, a range “of from 1 to 9” includes various individual integers, such as 3, as well as individual numbers including a decimal point (or fraction), such as 4.1, which may be relied upon and provide adequate support for specific embodiments within the scope of the appended claims.

The term “composition,” as used herein, includes material(s) which comprise the composition, as well as reaction products and decomposition products formed from the materials of the composition.

The term “comprising,” and derivatives thereof, is not intended to exclude the presence of any additional component, step or procedure, whether or not the same is disclosed herein. In order to avoid any doubt, all compositions claimed herein through use of the term “comprising” may include any additional additive, adjuvant, or compound, whether polymeric or otherwise, unless stated to the contrary. In contrast, the term, “consisting essentially of” excludes from the scope of any succeeding recitation any other component, step or procedure, excepting those that are not essential to operability. The term “consisting of” excludes any component, step or procedure not specifically delineated or listed. 

1. A composition for dispersing core shell particles, said composition comprising: an oligomer prepared from at least one alkyl (meth)acrylate monomer in the presence of a chain transfer agent, wherein the oligomer has a number average molecular weight of less than 2,500 g/mol.
 2. The composition of claim 1, wherein the oligomer has a number average molecular weight of less than 2,000 g/mol.
 3. The composition of claim 1, wherein the oligomer has a number average molecular weight of less than 1,750 g/mol.
 4. The composition of claim 1, wherein the oligomer has a degree of polymerization of less than
 25. 5. The composition of claim 4, wherein the oligomer has a degree of polymerization of less than
 20. 6. The composition of claim 1, wherein the at least one alkyl (meth)acrylate monomer comprises a monomer selected from ethyl (meth)acrylate, ethyl hexyl (meth)acrylate, and butyl (meth)acrylate.
 7. The composition of claim 1, wherein the chain transfer agent is selected from methyl 3-mercaptopropionate, butyl 3-mercaptopropionate, 2-ethyl hexyl thioglycollate, and pentaerythritol tetrakis(3-mercaptopropionate).
 8. A composition comprising a multilayer polymer and the composition according to claim
 1. 9. The composition according to claim 8, wherein the composition comprises the oligomer in an amount ranging from 2 to 98 wt % relative to the total weight of the oligomer and the multilayer polymer.
 10. The composition according to claim 8, wherein the multilayer polymer comprises a methacrylate butadiene styrene core shell polymer.
 11. The composition according to claim 8, wherein the composition is a powder.
 12. A resin composition comprising a resin selected from epoxy resin and methyl methacrylate resin, and the composition according to claim
 8. 13. The resin composition according to claim 12, wherein the resin composition comprises the oligomer in an amount ranging from 1 to 25 wt % relative to the total weight of the oligomer and the multilayer polymer.
 14. A process for improving dispersion of a multilayer polymer in a resin composition, comprising adding a powder composition according to claim 8 to a resin composition comprising a resin selected from epoxy resin and methyl methacrylate resin, wherein the dispersion of the multilayer polymer in the resin composition is improved relative to a similar resin composition that does not contain the oligomer. 